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On the use of molecular-based thermodynamic models to assess the performance of solvents for CO₂ capture processes: monoethanolamine solutions

机译:关于使用基于分子的热力学模型来评估溶剂对CO 2捕获过程的性能:单乙醇胺溶液

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摘要

Predictive models play an important role in the design of post-combustion processes for the capture of carbon dioxide (CO2) emitted from power plants. A rate-based absorber model is presented to investigate the reactive capture of CO2 using aqueous monoethanolamine (MEA) as a solvent, integrating a predictive molecular-based equation of state: SAFT-VR SW (Statistical Associating Fluid Theory-Variable Range, Square Well). A distinctive physical approach is adopted to model the chemical equilibria inherent in the process. This eliminates the need to consider reaction products explicitly and greatly reduces the amount of experimental data required to model the absorber compared to the more commonly employed chemical approaches. The predictive capabilities of the absorber model are analyzed for profiles from 10 pilot plant runs by considering two scenarios: (i) no pilot-plant data are used in the model development; (ii) only a limited set of pilot-plant data are used. Within the first scenario, the mass fraction of CO2 in the clean gas is underestimated in all but one of the cases, indicating that a best-case performance of the solvent can be obtained with this predictive approach. Within the second scenario a single parameter is estimated based on data from a single pilot plant run to correct for the dramatic changes in the diffusivity of CO2 in the reactive solvent. This parameter is found to be transferable for a broad range of operating conditions. A sensitivity analysis is then conducted, and the liquid viscosity and diffusivity are found to be key properties for the prediction of the composition profiles. The temperature and composition profiles are sensitive to thermodynamic properties that correspond to major sources of heat generation or dissipation. The proposed modelling framework can be used as an early assessment of solvents to aid in narrowing the search space, and can help in determining target solvents for experiments and more detailed modelling.
机译:预测模型在燃烧后过程的设计中发挥重要作用,以捕获发电厂排放的二氧化碳(CO2)。提出了一种基于速率的吸收器模型,以研究使用单乙醇胺水溶液(MEA)作为溶剂对CO2的反应性捕集,并结合了基于预测分子的状态方程:SAFT-VR SW(统计缔合流体理论-可变范围,方井) )。采用独特的物理方法来模拟过程中固有的化学平衡。与更常用的化学方法相比,这消除了明确考虑反应产物的需要,并大大减少了为吸收塔建模所需的实验数据量。通过考虑以下两种情况,对吸收器模型的预测能力进行了分析,以分析10个试验工厂运行的概况:(i)模型开发中未使用任何试验工厂数据; (ii)仅使用了一组有限的试验工厂数据。在第一种情况下,除一种情况外,在所有情况下均低估了清洁气体中CO2的质量分数,这表明采用这种预测方法可获得最佳的溶剂性能。在第二种情况下,将根据来自单个中试工厂运行的数据估算单个参数,以校正反应性溶剂中CO2扩散率的剧烈变化。发现该参数可在广泛的工作条件下转移。然后进行灵敏度分析,发现液体粘度和扩散率是预测组成曲线的关键特性。温度和成分曲线对热力学性质敏感,热力学性质对应于主要的热量产生或散发来源。所提出的建模框架可以用作溶剂的早期评估,以帮助缩小搜索空间,并可以帮助确定用于实验和更详细建模的目标溶剂。

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